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WO2009029087A2 - Hydrogels superporeux pour applications très résistantes - Google Patents

Hydrogels superporeux pour applications très résistantes Download PDF

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Publication number
WO2009029087A2
WO2009029087A2 PCT/US2007/072892 US2007072892W WO2009029087A2 WO 2009029087 A2 WO2009029087 A2 WO 2009029087A2 US 2007072892 W US2007072892 W US 2007072892W WO 2009029087 A2 WO2009029087 A2 WO 2009029087A2
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WO
WIPO (PCT)
Prior art keywords
hydrogel
acid
agent
sph
foaming
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Application number
PCT/US2007/072892
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English (en)
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WO2009029087A3 (fr
Inventor
Hossein Omidian
Jose Gutierrez-Rocca
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Abbott Laboratories
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Publication date
Application filed by Abbott Laboratories filed Critical Abbott Laboratories
Priority to CA2686927A priority Critical patent/CA2686927A1/fr
Priority to EP07875165A priority patent/EP2073792A2/fr
Priority to JP2009530490A priority patent/JP2009542895A/ja
Priority to MX2009000046A priority patent/MX2009000046A/es
Publication of WO2009029087A2 publication Critical patent/WO2009029087A2/fr
Publication of WO2009029087A3 publication Critical patent/WO2009029087A3/fr

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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/06—Ointments; Bases therefor; Other semi-solid forms, e.g. creams, sticks, gels
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/02—Inorganic compounds
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/30—Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
    • A61K47/32—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. carbomers, poly(meth)acrylates, or polyvinyl pyrrolidone
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F251/00—Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/01—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to unsaturated polyesters
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F289/00—Macromolecular compounds obtained by polymerising monomers on to macromolecular compounds not provided for in groups C08F251/00 - C08F287/00
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F290/00—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups
    • C08F290/02—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups on to polymers modified by introduction of unsaturated end groups
    • C08F290/06—Polymers provided for in subclass C08G
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F291/00—Macromolecular compounds obtained by polymerising monomers on to macromolecular compounds according to more than one of the groups C08F251/00 - C08F289/00
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/003—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to macromolecular compounds obtained by reactions only involving unsaturated carbon-to-carbon bonds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/02—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to polysaccharides

Definitions

  • the present invention relates to methods for the formation of superporous hydrogels having improved physical and mechanical properties.
  • Superporous hydrogels are porous networks of hydrophilic and/or hydrophobic polymer chains. SPHs contain a multiplicity of pores with diameters in the micrometer to millimeter range, which enable them to absorb tens of times their weight of aqueous fluids in just a fraction of a minute in a manner that is independent of their size in the dehydrated state, SPH pores are interconnected in the hydrogel matrix such that absorbing fluid can move freely through the channels (capillaries). These interconnecting pores allow the SPHs to swell much faster than conventional hydrogels that have the same swelling capacity.
  • U.S. Patent No. 6,271 ,278 describes the preparation of various SPHs in detail. SPHs are also described by Chen, et al., in J Biomed Mater Res 44:53-62, 1999.
  • SPHs are generally prepared based on hydrophilic monomers, including acrylic acid and its salts, acrylamide, the potassium salt of sulfopropyl acrylate, hydroxyethyl acrylate, and hydroxyethyl methacrylate.
  • the hydrophilic or hydrophobic nature of the primary monomer can control the SPH's properties, including swelling (capacity and rate) and mechanical properties (elasticity, compressive strength, and resiliency)
  • swelling is favored by the presence of either ions in the polymer backbone (e.g., ionic monomers) or hydrophilic functional groups in the polymer, such as, for example, hydroxy!, carboxyl, amide, and amino groups.
  • ions in the polymer backbone e.g., ionic monomers
  • hydrophilic functional groups in the polymer such as, for example, hydroxy!, carboxyl, amide, and amino groups.
  • These hydrogels can swell to a very large size in a very short period of time. In contrast to their superior swelling properties, these hydrogels frequently suffer from weak mechanical properties. Conversely, enhanced mechanical properties can be achieved with less hydrophilic superporous hydrogels at the expense of favorable swelling properties
  • SPH gastric retention
  • the SPH must be able to swell to a size sufficient to delay release of the SPH from the stomach via the pyloric sphincter. It is generally thought that for oral dosage forms to remain in the stomach in the fasted state, their dimensions must be 15 mm or larger. Further, fasted state gastric conditions are characterized by an environment of greatly increased mechanical and chemical stress. Accordingly, a suitable SPH must be strong enough to resist the acidic conditions in the stomach as well as the pressures that occur during stomach contractions, which can exhibit maximum pressures in the range of 100 to 130 cm H 2 O.
  • This invention features superporous hydiogels (SPHs) with stable physical and mechanical properties, and methods for preparing SPHs having these properties.
  • the desirable properties are achieved by controlling the hydrophilicity/hydrophobicity of the SPH structure and by harmonizing the foaming/polymerization conditions during SPH formation.
  • a first aspect of the invention features a method of preparing a superporous hydrogel by a) preparing a mixture that includes an ethyle ⁇ ically-unsaturated monomer of hydroxyethyl methacrylate (HEMA).
  • HEMA hydroxyethyl methacrylate
  • the property-modifying agent has an ion-complexable site.
  • the mixture of step a) includes at least one property-modifying agent has an ion- complexable site comprising an ion selected from (e g., H + , Na + , K + , NHL) + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , Mn 2+ , Fe 2+ , Fe 3+ , Cr 3+ , Al 3+ , or Ce 4+ ).
  • an ion selected from e g., H + , Na + , K + , NHL
  • the property-modifying agent is selected from a monomer, e.g , an acrylic acid; a polymer; and a polyphenols complexing agent.
  • the mixture of step a) further includes one or more of a diluent, a foaming agent, a foaming aid, and a foam-stabilizer.
  • the foaming agent can be added as a solid mass; dissolved in an aqueous or organic/aqueous solvent system; dispersed in an organic solvent; coated with an organic compound such that dissolution of said foaming agent in water is delayed; encapsulated such that dissolution of said foaming agent in water is delayed; or dispersed in a monomer that participates in the superporous hydrogel polymerization.
  • Polymerization of the hydrogel includes subjecting the mixture to foaming conditions substantially concurrently with gelation of the hydrogel
  • the mixture of step a) further includes a foaming agent and a foaming aid, in which the foaming aid reacts with the foaming agent within between 5 and 15 seconds after its addition to the mixture.
  • the mixture of step a) can additionally include one or more ethylenically unsaturated comonomers, which are present in the mixture in less than 20 wt%.
  • the polymerization step b) occurs at a temperature in the range of about 20 0 C to about 100 0 C. In another embodiment, the temperature is in the range of about 55 0 C to about 75 0 C. Alternatively, the temperature can be in the range of about 30 0 C to about 60 0 C.
  • the method further includes c) reacting the hydrogel with one or more ions (e.g., H + , Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2 ⁇ , Mn 2+ , Fe 2+ , Fe 3+ , Cr 3 ' , A1 3 ⁇ or Ce 4+ ) under equilibrating conditions.
  • one or more ions e.g., H + , Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2 ⁇ , Mn 2+ , Fe 2+ , Fe
  • the mixture of step c) can also include a chelating agent, e g., a monovalent, bivalent, or trivalent ion salt).
  • the chelating agent can be selected from potassium chloride, calcium chloride, and aluminum chloride.
  • the hydrogel may further be treated with one or more ions (e.g., H + , Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , Mn 2+ , Fe 2+ , Fe 3+ , Cr 3+ . Al 3+ , or Ce 4+ ) under equilibrating conditions.
  • one or more ions e.g., H + , Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , Mn 2+ , Fe 2+ , Fe 3+ , Cr 3+ . Al 3+ , or Ce 4+
  • the temperature of the mixture is preferably maintained at between about 2O 0 C and about 8O 0 C, more preferably between about 2O 0 C and about 60 0 C, and most preferably between about 20 0 C and about 4O 0 C.
  • the hydrogel is dehydrated, e.g., by lyophilization.
  • Lyophilization of the hydrogel can be performed by (a) freezing the hydrogel at a temperature in the range of 23 0 C to -1O 0 C with a cooling rate of between about I 0 C and about 5 0 C per hour; (b) maintaining the hydrogel at a temperature in the range of about - 5 0 C to about -2O 0 C for between about 16 to about 24 hours; (c) lyophilizing the sample at a temperature in the range of about -5 0 C to about -2O 0 C and a pressure of less than about 0.2 Torr for between about 60 and about 80 hours; (d) increasing the sample temperature to between about 5 0 C and about 15 0 C at a rate of between about I 0 C and about 5 0 C per hour; and (e) maintaining the sample at a temperature in the range of about 5 0 C and about 15 0 C and at a pressure of less than about 200 mTorr for between about 8 to about 48 hours.
  • the preventative layer prevents migration and/or direct contact of the plasticized hydrogel with the capsule
  • the plasticized hydrogel is treated with a coating agent, which can be applied to the hydrogel prior to encapsulation, which prevents the plasticizer from contacting the capsule.
  • the hydrogel can be plasticized by exposing the hydrogel to a high relative humidity environment (e.g., greater than about 60% relative humidity) and at a temperature above about 37 0 C (e.g.. a temperature about 4O 0 C, about 5O 0 C, or about 6O 0 C).
  • the hydrogel includes a fast moisture- absorptive agent that catalyzes plasticization of the hydrogel.
  • a second aspect of the invention features a superporous hydrogel prepared by the method of the first aspect of the invention.
  • the hydrogel exhibits improved strength and mechanical properties (e.g., the ability to resist a compressive load of between about 2 to about 50 N; and the ability, when in its fluid- swollen state, to maintain its mechanical integrity at a pH less than about 5.0, more preferably less than about 3.0, and most preferably less than about 1.0, preferably for greater than 1 hour and most preferably for greater than 3 hours).
  • the hydrogel when it its dry state, has an average pore size in the range of about 1 ⁇ m to about 5000 ⁇ m, preferably in the range of about 10 ⁇ m to about 3000 ⁇ m.
  • the relative compressive strength of the superporous hydrogel is about 5-fold greater than the compressive strength of a superporous hydrogel lacking a property-modifying agent and the compressive strength at breaking point of the superporous hydrogel, when in its fluid-swollen state, is between about 1.0 kPa and about 500 kPa, more preferably between about 100 kPa and about 500 kPa.
  • the equilibrium volume swelling ratio of the superporous hydrogel is in the range of about 8 to 18 (swollen: unswollen).
  • a third aspect of the invention features a pharmaceutical composition in solid dosage form that includes a pharmacologically effective dose of a biologically active agent and the superporous hydrogel prepared by the method of the first aspect of the invention.
  • the biologically active agent is a drug, a nutritional supplement, or a fertilizer and the solid dosage form can be selected from a tablet, a capsule, particles, a wax, oil, granules, a film, a sheet, a fiber, a rod, and a tube.
  • the tablet or capsule is formed by a molding, by direct compression, or by using a press coating compression technique.
  • a fourth aspect of the invention features a method for prolonged retention of a pharmaceutical agent (e.g., a drug or a nutritional supplement, such as a vitamin) by gastric retention.
  • the method includes administering to a patient a superporous hydrogel prepared by the method of the first aspect of the invention that includes the pharmaceutical agent; the hydrogel swells upon entering the stomach of the patient and extends release of the agent for at least one hour.
  • a pharmaceutical agent e.g., a drug or a nutritional supplement, such as a vitamin
  • cation-complexable site is meant a position in a molecule capable of forming a reversible association with another molecule, an atom, or an ion through a non- covalent chemical bond .
  • crosslinking agent is meant a molecule able to form a chemical bond to another substrate in the formation of a matrix.
  • hydrogel is meant a crosslinked polymer network that is not soluble in water but swells to an equilibrium size in the presence of aqueous fluids.
  • peptide is meant a molecule that contains from 2 to 100 natural or unnatural amino acid residues joined by amide bonds formed between a carboxyl group of one amino acid and an amino group from the next one.
  • functionalized peptide refers to those peptides that have at least two groups suitable for carrying out a crosslinking reaction These groups include olefins, carbonyls, esters, acyl halides. alkyl halides, and the like.
  • protein is meant a molecule that contains greater than 100 natural or unnatural amino acid residues joined by amide bonds formed from a carboxyl group of one amino acid and an amino group from the next one.
  • functionalized protein refers to those proteins that have at least two groups suitable for carrying out a crosslinking reaction. These groups include olefins, carbonyls, esters, acyl halides, alkyl halides, and the like.
  • “superporous hydrogel” is meant a hydrogel that has interconnecting pores.
  • the pores can be in excess of 1 ⁇ m, 1 O ⁇ m, 100 ⁇ m, 200 ⁇ m, 300 ⁇ m, 400 ⁇ m, 500 ⁇ m, or up to the millimeter range.
  • Figure 5 is a graph showing SPH mechanical property and homogeneity for a p(HEMA)-based SPH synthesized at a starting reaction temperature of 6O 0 C, and swelling at 37 0 C for 4 hours in a simulated gastric fluid swelling medium.
  • Figure 6 is a graph showing SPH mechanical property and homogeneity for a p(HEMA/HEA)-based SPH synthesized at a starting reaction temperature of 60 0 C, and swelling at 37 0 C for 4 hours in a simulated gastric fluid swelling medium.
  • Figure 7 is a graph showing the effects of different starting reaction temperatures on the mechanical properties of a p(HEMA)-based SPH. in a deionized water swelling medium at 22-25 0 C for 4 hours.
  • Figure 8 is a graph showing the effects of different starting reaction temperatures on the mechanical properties of a p(HEMA)-based SPH, in a simulated gastric fluid swelling medium.
  • Figure 9 is a graph showing the effects of using HEA as a co-monomer on the " mechanical properties of a p(HEMA)-based SPH.
  • Figure 10 is a graph showing the effects of different swelling media on the mechanical properties of a p(HEMA)-based SPH synthesized at 60 ° C
  • Figure 11 is a graph showing the alcohol absorption capabilities of a p(HEMA)- based SPH.
  • Figures 12 and 13 are graphs showing the effects of different cyclic compression loadings on the mechanical properties of a p(HEMA)-based SPH.
  • the present invention features SPHs having unique mechanical properties and swelling ability (e.g., high compressive strength with minimal diffusion and maximum capillary absorption during absorption of fluids)
  • SPHs of the present invention are prepared using a less hydrophilic monomer, e.g., hydroxyethyl methacrylate (HEMA) or similar, which can provide a sponge like material with certain beneficial hydrogel properties via a reduction in the absorption of water.
  • HEMA hydroxyethyl methacrylate
  • the HEMA monomer can be formulated to polymerize at room or high temperature using, e.g., thermal or redox polymerization initiators.
  • SPH formulations of the present invention can contain high amounts of crosslinker, which produces SPHs having an enhanced elastic property in their swollen state.
  • a property modifier having chelating ability can be incorporated into the hydrogel network as a minor component. Adjusting the temperature at which the polymerization reaction is started also improves the porous structure and homogeneity of the SPH.
  • the SPHs of the present invention which are modified polyHEMA SPHs, exhibit improved mechanical integrity and swelling abilities for extended periods of time (e.g., 1 to 5 hours) at all pH values tested, but especially when tested in a very harsh swelling environment, such as simulated gastric fluid (SGF) at a pH of 1 0.
  • SGF simulated gastric fluid
  • the dehydrated SPHs of the present invention lapidly swell to a relatively large size when placed in contact with aqueous fluids, yet remain mechanically strong in their swollen state over prolonged periods of time, e.g., up to 4 hours.
  • the present invention features methods for the preparation of these SPHs 5 which include choosing proper formulation and reaction conditions to obtain a very strong and non-reflexive SPH.
  • the SPHs of the present invention in their fully swollen state, are able to resist static and dynamic loadings in the range of 0, 1 to 50 Newtons, the higher range being well above the requirements for all but the most rigorous pharmaceutical or biomedical applications
  • an ethylenically-unsaturated monomer preferably 2-hydroxyethyl methacrylate (HEMA)
  • HEMA 2-hydroxyethyl methacrylate
  • one or more co-monomers comprising ion-complexable sites
  • one or more ciosslinkers diluents
  • surfactants e.g., surfactants, foaming agents, foaming aids, and initiators
  • foaming agents e.g., 85, 90, or 95 wt%.
  • alkylamides of methacrylic acid C 2 - I2 dialkylamides of methacrylic acid, N-cyclopropyl methacrylamide, N t N-dimethylaminoethyl acrylate, acrylonitrile, 2-hydroxyethyl acrylate (HEA), ethyl acrylate, butyl acrylate, isodecyl methacrylate, methyl methacrylate, lauryl methacrylate, stearyl methacrylate, 2-hydroxypropyl acrylate.
  • HOA 2-hydroxyethyl acrylate
  • the concentration of comonomer is from about 0.5% to about 20% (v/v), preferably about 5% to about 15% (v/v), and most preferably about 10 % (v/v), of the total reaction mixture when present.
  • the reaction mixture includes 2- hydroxymethyl methacrylate (HEMA) as a primary monomer and a comonomer selected from one or more of AAm, NIPAM, Methacrylic Acid, AAC, or salts thereof, DADMAC, or SPMAK.
  • HEMA 2- hydroxymethyl methacrylate
  • Crosslinking agents can be N, N'- methyl enebisacrylamide (BIS), N t N'- ethylenebisacrylamide (EBA), polyethylene glycol diacrylate (PEGDA), polyethylene glycol dimethacrylate (PEGDMA), ethylene glycol diglycidyl ether, alkoxylated cyclohexanedimethanol diacrylate, dipentaerythritol pentaacrylate, ethoxylated (9) trimethylolpropane triacrylate, ethoxylated (15) trimethylolpropane triacylate, methoxy polyethylene glycol (550) monomethacrylate, ethoxylated hydroxyethyl methacrylate, methoxy polyethylene glycol (350) methacrylate, glycidyl methacrylate, polyamidoamine epichlorohydrin resin, trimethylolpropane triacrylate (TMPTA), piperazine diacrylamide, glutaraldehyde, or epichlor
  • the volume/volume ratio of crosslinker to monomer is from about 0.01/100 to about 1/10. Most desirably, the volume/volume ratio of crosslinker to monomer is from about 1/100 to 5/100. Desirably, the crosslinker is PEGDA.
  • Diluents that can be used to form a SPH of the present invention include deionized water (DI) any organic solvent in water, or any alcohol, including, e.g., ethyl alcohol and isopropyl alcohol (IPA)
  • DI deionized water
  • IPA isopropyl alcohol
  • Useful organic solvents include methanol, ethanol, 1-propanol, 2-propa ⁇ ol, tetrahydrofuran, dioxane, formic acid, acetic acid, acetonitrile, nitromethane, acetone, or 2-butanone.
  • the non-aqueous solvent is ethanol
  • a foaming agent can be added to the reaction mixture as a solid mass or it can be dissolved in an aqueous or organic/aqueous solvent system; dispersed in an organic solvent; coated with an organic compound such that dissolution of the foaming agent in water is delayed; encapsulated such that dissolution of the foaming agent in water is delayed; or dispersed in a monomer that participates in polymerization of the SPH.
  • Foaming agents include physical agents that expand when pressure is released, such as nitrogen and carbon dioxide, and chemical agents, which decompose or react, e.g , in the presence of an acid, to form a gas, e.g., azodiacarbonamide, NaHCC> 3 , Na 2 COs, and CaCO 3
  • Inorganic carbonates such as sodium carbonate, potassium carbonate, ammonium carbonate, calcium carbonate, potassium bicarbonate, ammonium bicarbonate, or, most desirably, sodium bicarbonate, are preferred for use as a foaming agent.
  • the weight (in mgs) to volume (in ⁇ L) ratio of foaming agent to monomer is from about 0.1/100 to about 2/5. Most desirably, the w/v ratio of foaming agent to monomer is about 1/7
  • Foaming aids are used in combination with the foaming agent for the generation of gas.
  • Foaming aids include organic and inorganic acids, such as, for example, acrylic acid, citric acid, acetic acid, phosphoric acid, carbonic acid, boric acid, sulfuric acid, p- toluene sulfonic acid, nitric acid, hydrobromic acid, chloric and hydrochloric acid.
  • An example of a preferred foaming aid is glacial acetic acid.
  • the volume/volume or weight (in mgs) to volume (in ⁇ L) ratio of foaming aid to monomer is from about 0 01 / 100 to about 1/10
  • the v/v or w/v ratio of foaming aid to monomer is from about 1/100 to 5/100
  • the SPH reaction mixture can also include one or more property-modifying agents, e.g., agents that contain cation-complexable sites
  • Property-modifying agents include, e.g., monomers, such as acrylic acid, polymers (e.g., a polysaccharide selected from alginate and derivatives thereof, chitins, chitosan and derivatives thereof, cellulose and derivatives thereof, starch and derivatives thereof, cyclodextrin, dextran and derivatives thereof, gums, lignins, pectins, saponins, deoxyribonucleic acids, and ribonucleic acids; a polypeptide or protein selected from albumin, bovine serum albumin, casein, collagen, fibrinogen, gelatin and derivatives thereof, gliadin, sodium glycine carbonate, bacterial cell membrane enzymes, and a poly(amino acid), in particular polyproline, poly(L-arginine), poly(L-lysine), polysarco
  • the property-modifying agent is selected from carboxymethylcellulose, alginate, starch glycolate, carboxymethyl starch, dextran, pectinate, xanthan, carrageenan, gellan, hyaluronic acid, and pectinic acid, or salts thereof, wherein the salt includes a counterion selected from Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , and Mn 2+ , and poly(acrylic acid) and its salts, poly(methacrylic acid) and its salts, polyacrylamide, poly(styrene sulfonate), poly(aspartic acid), polylysine, CARBOPOL, and ultramylopectin.
  • the salt includes a counterion selected from Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , and Mn 2+
  • Preferred polysaccharides include, e.g., ionic polysaccharides having negatively/positively charged groups that can counter the positive/negative charge of a cation/ anion.
  • a primary cation is initially provided with the ionic polysaccharide of the SPH formulation, with the polysaccharide playing a critical role in the process of subsequent ion-equilibration(s).
  • the polysaccharide is chosen from the list that includes alginate and derivatives thereof, chitins, chitosan and derivatives thereof, cellulose and derivatives thereof, such as carboxymethylcellulose, starch and derivatives thereof, such as starch glycolate and caiboxymethyl starch, dextran and derivatives thereof, such as cyclodextrin and dextran sulfate, gums, lignins, pectins, pectinate, saponins, hyaluronic acid, xanthan, carrageenan, gellan, and alginate, or a salt thereof, wherein the salt comprises a counterion selected from Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+ , Cu 2+ , Zn 2+ , and Mn 2+ .
  • the salt comprises a counterion selected from Na + , K + , NH 4 + Ca 2+ , Mg 2+ , Ba 2+
  • the polysaccharide is sodium carboxymethylcellulose.
  • the ratio of polysaccharide to total solution can be in the range of about O 1 to about 10% w/v Preferably, the range is about 0.2 to about 5% w/v. Most preferably, the range is about 0.2 to about 1.5% w/v.
  • Preferred polypeptide or proteins include albumin, bovine serum albumin, casein, collagen, fibrinogen, gelatin and derivatives thereof, gliadin, sodium glycine carbonate, bacterial cell membrane enzymes, and a poly(amino acid), such as polyproline, poly(L- arginine), poly(L-lysine), polysarcosine, poly(L-hydroxyproline), poly(glutamic acid), poly(S-carboxymethyl-L-cysteine), and poly(aspartic acid).
  • a poly(amino acid) such as polyproline, poly(L- arginine), poly(L-lysine), polysarcosine, poly(L-hydroxyproline), poly(glutamic acid), poly(S-carboxymethyl-L-cysteine), and poly(aspartic acid).
  • the polyphenols complexing agent can be selected from any one of the following: gallotannins, ellagitannins, taragallotannins, caffetannins, proanthocyanidins, catechin, epicatechin, chlorogenic acid, and arbutin.
  • foam stabilization can be accomplished by physical or chemical means.
  • a rapid cooling or hot drying (for example, flash drying at a high temperature under an inert atmosphere) process can be used to stabilize the foam that has been produced by a gas blowing technique.
  • Surfactants for use in preparing the SPHs of the present invention include any composition that, when dissolved in a liquid, reduces the surface tension of the liquid to the extent that a gas can be introduced into the liquid solution of the surfactant to form a foam.
  • a surfactant can be used to stabilize the foam until the beginning of the gelling process.
  • Useful surfactants include chemical surfactants, such as Triton surfactants, Tween and Span surfactants, Pluronic ® surfactants (poly(ethylene oxide)-poly(propylene oxide)- poly(ethylene oxide) tri-block copolymers) (BASF), Silwet ® surfactants (OSi Specialties Inc.), and sodium dodecyl sulfate (Bio-Rad Laboratories), and proteinaceous surfactants, such as albumin (Sigma Chemical Company), ovalbumin, gelatin, or combinations thereof.
  • Pluronic ® F 127 PF 127) is used.
  • surfactant concentrations in the range of about 0.2% to about 2% (w in gms/v in mLs) of the total solution were found to be adequate.
  • the surfactant concentration is in the range of about 0.4% to about 1% (w in gms/v in mLs).
  • the surfactant concentration is about 0.9% (w in gms/v in mLs).
  • Polymerization of SPHs may be initiated by any polymerization-initiator system that is suitable for the polymerization of unsaturated monomers in the homogeneous or heterogeneous phase.
  • initiator systems that may be used in the process according to the present invention are those known to the person skilled in the art (see, e.g., U.S. Patent Nos. 6,960.617; 6,271,278; and 5,750,585; and U.S. Patent Application Publication Nos. US 2003/0232895 and US Patent No. 7,056,957; each of which is incorporated herein by reference).
  • polymerization occurs at a temperature in the range of about 20° to about 100 0 C, preferably in the range of about 30° to about 60 0 C.
  • such polymerization initiators are desirably free-radical or free-radical forming compounds or mixtures of substances, such as, for example, hydroperoxides, preferably cumyl hydroperoxide and tert.-butyl hydroperoxide; organic peroxides, preferably dibenzoyl peroxide, dilauryj peroxide, dicumyl peroxide, di-tert.-butyl peroxide, methyl ethyl ketone peroxide, tert- butylbenzoyl peroxide, diisopropyl peroxydicarbonate, or dicyclohexyl peroxydicarbonate, di-tert-butyl peroxalate; inorganic peroxides, preferably ammonium persulfate, potassium persulfate, potassium peroxydisulfate, or hydrogen peroxide; azo compounds, preferably azobis(isobutyronitrile), l,l'-azo
  • the initiator systems can be pure or in the form of mixtures of two, three or more different initiator systems.
  • portions of the initiator system are added to the reaction separately in solid, liquid or gaseous form. This procedure is particularly suitable for redox initiator systems.
  • a combination of an oxidant and a reductant (a redox pair) is desirable as an initiator.
  • the redox pair of ammonium persulfate (APS) and N.N.N'.N'-tetramethylethylenediamine (TEMED) is used
  • APS ammonium persulfate
  • TEMED N.N.N'.N'-tetramethylethylenediamine
  • SPH's of the present invention can be formed using a thermal initiator of polymerization, such as a thermally decomposable initiator (e.g., ammonium perfulfate).
  • the SPHs of the present invention are formed using combined thermal and redox initiator systems
  • Ion equilibration is a process by which ion exchange happens within the substrate structure
  • the exchange process may take place between any kinds of ions of different valences (e.g., monovalent, divalent, trivalent or higher).
  • bivalent cations within the substrate can partially be replaced by trivalent cations or vice versa.
  • the SPH product contains equilibrium amounts of two or more cations.
  • the equilibration just described results in considerable change in substrate properties. For example, sodium salt of carboxymethylcellulose is soluble in water, while its calcium-treated derivative is water-insoluble.
  • a SPH of the present invention can originally contain ions or can be ionized after its formation.
  • the SPH may contain a primary cation selected from a salt, ionic monomer, ionic polymer, oi any other ionic ingredient.
  • the primary cation can be subsequently partially or completely replaced by another cation, i.e., a secondary cation.
  • An equilibrium mixture of primary and secondary cations can also be equilibrated with a third cation, i.e., tertiary cation, and so on.
  • the process of ion-equilibration can be repeated with a number of different cations.
  • a simple salt, ionic monomer, ionic polymer or another ion source can provide the secondary or tertiary cation.
  • the ion-equilibration process can take place in an aqueous or a mixed aqueous/alcoholic medium, where the ions can move with freedom
  • an ion-bearing SPH can be immediately placed into an aqueous or mixed aqueous/alcoholic solution that includes any monovalent, bivalent, or trivalent cations, or mixture thereof, or of higher-valent cations, e.g., cerium.
  • the monovalent cation is H + , Na + . K + , or NH4 +
  • the bivalent cation is Ca 2+ , Ba 2+ , Mg 2+ , Cu 2+ , Zn 2x , Mn 2+ , or Fe 2+
  • the bivalent cation is Ca 2+ .
  • the trivalent cation is Fe 3+ , Cr 3" ", or Al 3 ⁇ .
  • the ion-exchange process between monovalent and bivalent cations is rapid as fast swelling of the SPH significantly decreases the time required for this exchange/equilibration. Although the process of ion-equilibration is fast, to ensure that
  • the ion-equilibrated SPH may be retreated with a solution that includes a tertiary cation.
  • the trivalent cation is iron or aluminum.
  • the SPH is placed into medium that includes a trivalent cation and cation equilibration occurs rapidly.
  • the hydrogel is left in the solution for period of time, preferably from about 0.5 hour to about 24 hours.
  • the equilibration process occurs at a temperature of between about 20° to about 60 0 C, more preferably between about 20° to about 35 0 C.
  • the influence of cations on SPH properties is disclosed in. e g.. U.S. Patent Application Publication No. US Patent No. 7,056,957 (see Table 1)
  • the ion-equilibrated hydrogel is then thoroughly washed with pure water, washed with a non-aqueous, water-miscible solvent, and dried out in an oven or in a vacuum oven.
  • the purified superporous hydrogel can be dried out in an oven/vacuum oven or by a lyophilization technique.
  • the SPHs of the present invention are normally dehydrated and stored before use.
  • one method that can be utilized includes the steps of, (a) freezing the SPH sample at a temperature of about 23 0 C to about -1O 0 C with a cooling rate of about 3 0 C pei hour, (b) maintaining the sample at about -1O 0 C for about 16 to about 24 hours, (c) lyophilizing the sample at about -10 0 C and at less than about 0.2 Torr for about 60 to about 80 hours, (d) increasing the sample temperature to about 10 0 C at a rate of about 3 0 C per houi, and (e) maintaining the sample at about 10 0 C and at less than about 200 mTorr foi at least about 12 hours.
  • a desirable method includes the steps of (a) displacing water contained in the hydrogel matrix with a non-aqueous, water-miscible solvent or solvent mixture through a series of washings, and (b) removal of the non-aqueous solvent or solvent mixture at a pressure of less than about 50 Toir or by heat
  • the non-aqueous solvent can include methanol, ethanol, 1-propanol, 2-propanol, tetrahydrofuran, dioxane, formic acid, acetic acid, acetonitriie, nitromethane, acetone, or 2-butanone.
  • the non-aqueous solvent is ethanol ,
  • SPHs of the invention can be used in a variety of different applications owing to the unique properties exhibited by these SPHs over other hydrogels, including other SPHs that are manufactured without the incorporation of HEMA.
  • the SPH can be in any form, including but not limited to a film, sheet, particle, granule, fiber, rode or tube,
  • the SPHs of the present invention are extremely useful in drug delivery, desirably, for use as an oral pharmaceutical agent.
  • Drug delivery can involve implanting a controlled release drug or drug composition within a matrix of a dehydrated SPH of the present invention This, in turn, would be contained in a capsule (e.g., a gelatin capsule) or similar housing system that can be eroded by the acidic conditions in the stomach.
  • SPHs gastric retention of SPHs is based on their unique swelling properties, i.e., fast swelling to a large size. Once a SPH of the present invention is exposed to gastric fluid, it rapidly swells to its maximum swelling capacity, typically in less than ten minutes. For their use in humans, SPHs that swell to a diameter of greater than about 2 cm at low pH conditions are desirable as they are then unable to pass through the pylorus sphincter, ensuring prolonged residence in the stomach and better absorption of the drug.
  • the SPHs of the present invention can have a variety of other applications including, for example, tissue engineering, vascular surgery (e.g., angioplasty) and drainage (e.g., from the kidney).
  • Devices prepared using SPHs of the present invention can include, but are not limited to, vascular grafts, stents, catheters, cannulas, plugs, constrictors, tissue scaffolds, and tissue or biological encapsulants, and the like.
  • the SPHs of the piesent invention may be applied to any use that requires a porous hydrogel material, particularly a use that requires a hydrogel material having an open pore structure.
  • the materials are useful as matrices or scaffolds into which cells can migrate, the cells being compatible therein and growing to achieve their intended function, such as in tissue replacement, eventually replacing the matrix depending on its biodegradability.
  • the materials can be used to provide matrices already bound to cells, which may then be surgically implanted into a body. Further, the materials can be used as wound healing matrix materials, as matrices for in vitro cell culture studies or uses similar thereto.
  • the SPHs of the present invention are ideal for use in culturing cells owing to their stable structure.
  • SPHs of the present invention can also be used to create three-dimensional tissues that include, e.g., smooth muscle cells, especially if appropriate cell adhesion ligand(s) are coupled to the SPH.
  • the SPHs of the present invention can incorporate growth factors.
  • the SPHs of the present invention can be used to provide a suitable environment for cell proliferation.
  • GTR guided tissue regeneration
  • absorbent article is meant a consumer product that is capable of absorbing significant quantities of water and other fluids (i.e., liquids), e.g., body fluids.
  • absorbent articles include disposable diapers, sanitary napkins, incontinence pads, paper towels, facial tissues, and the like.
  • SPHs of the present invention are also useful for protecting, holding or transplanting growing plants in the form of seeds, seedlings, tubers, cuttings, nursery stock, roots, transplants and the like. These SPHs can aid a growing plant, either alone or in combination with fertilizer, agricultural modified minerals, and the like uniformly dispersed throughout.
  • SPHs of the present invention are also useful for adsorption, extraction, separation, and filtration purposes.
  • the SPHs can be used as a desiccant to remove moisture ftom the surrounding environment.
  • the SPHs of the present invention can be used to separate water from mixtures containing, e.g., mixed water/oil, water/alcohol, water/organic solvents, and similar.
  • SPHs of the present invention exhibit several improved characteristics, including, e.g., prolonged stable swelling and mechanical properties in their swollen state (e.g.. when swollen in very harsh swelling medium, such as stimulated gastric fluid), and structural homogeneity.
  • the equilibrium volume swelling ratio of SPHs of the present invention falls within the range of about 8 to about 18 (swollen volume to unswollen volume).
  • SPHs of the present invention can also withstand greater compressive loads, e.g., a compressive load of 10 N or greater (e g., a compressive load in the range of about 10 N to about 50 N).
  • the SPHs of the present invention also retain their mechanical integrity under the swelling conditions found in the environment of the stomach, i.e., swollen with gastric fluid, and the compressive loads applied by the stomach.
  • the SPH can retain its mechanical integrity at a pH of less about 5.0, more preferably at a pH of about 3.0, and most preferably at a pH of about 1.0, for at least greater than one hour and more preferably for greater than three hours.
  • the SPHs of the present invention that include one or more property-modifying agents, such as the ones described above, can withstand a compressive load of at least about 5-fold greater, more preferably at least about 10-fold greater, and most preferably at least about 20-fold greater, than SPHs prepared without the property-modifying agent(s).
  • the SPHs of the present invention exhibit an average pore size of about 1 ⁇ m to about 5.000 ⁇ m. More preferably, the SPHs exhibit an average pore size of about 10 ⁇ m to about 3,000 ⁇ m
  • the pore size of the SPH critically affects the SPH properties. Conditions such as higher reaction temperature, higher water content of the reacting medium, and higher concentration of foaming components results in a taller foam with higher swelling, better processability, and lower mechanical properties in the swollen state. A shorter foam exhibits larger pore sizes and more rigidity in the swollen state
  • the methods of the present invention yield a very processable poJyHEMA-based SPH product that can be prepared using a high starting reaction temperature.
  • the SPH can be processed into a very thin hydrogel in its swollen form.
  • the preparation of an polyHEMA SPH of the present invention using a high starting reaction temperature results in a veiy homogeneous porous structure having smaller pores, more flexibility in the swollen state, and faster absorption rates, and which can be easily purified.
  • the polyHEMA SPH of the present invention behaves like a sponge for water and absorbs water mostly via a capillary mechanism.
  • the foaming and polymerization reactions are simultaneously controlled ('harmonized')- This is done by monitoring the time/temperature profile during SPH formation and noting the progress of the foaming process.
  • HEMA hydroxyethyl methacrylate
  • PEGDA polyethyleneglycol diacrylate
  • acrylic acid 50 ⁇ L
  • acetic acid 40 ⁇ L
  • F127-10% 250 ⁇ L
  • TMED-40% tetramethyl ethylenediamine
  • APS-10% APS-10%, 250 ⁇ L
  • the temperature of this profile starts at 25 0 C. After an induction period of about 100 sec, the reaction starts and continues smoothly over the next 400 sec, with a linear increase of temperature to about 55 0 C. During this time it was observed that the viscosity of the reaction mixture increased slightly. The reaction then becomes vigorous, with a sharper linear increase in temperature over the next 100 seconds. During this time the solution turns quickly to a turbid mass.
  • the SPH prepared using this formulation exhibits improved strength and mechanical properties.
  • FIG. 3 is a graph showing the results of an evaluation of a pHEMA SPH prepared by the method described above, except that the SPH was prepared at a starting reaction temperature of 60 0 C. The SPH, once formed, was tested using a Chatillon TCD- 200 digital mechanical tester. The SPH was swollen using deionized water as the swelling medium at a temperature of 22-25 0 C The SPH was retained in the swelling medium for at least 4 hrs before mechanical testing.
  • Figure 4 is a graph showing the results of an evaluation of a pHEMA SPH prepared by the method described above. Swelling of the SPH was performed using simulated gastric fluid at a pH of 1 0 at 37 0 C for 0.5 hr. The SPH was prepared at a starting reaction temperature of 6O 0 C. The SPH, once formed, was tested using a Chatillon TCD-200 digital mechanical tester.
  • FIG. 5 is a graph showing the results of an evaluation of a pHEMA SPH prepared by the method described above.
  • Swelling of the SPH was performed using simulated gastric fluid at a pH of 1.0 at 37 0 C for 4 hr.
  • the SPH was prepared at a starting reaction temperature of 6O 0 C.
  • the SPH, once formed, was tested using a Chatillon TCD- 200 digital mechanical tester. Testing of the SPH was as follows: a cylindrical dehydrated SPH sample was placed into SGF at 37 0 C for about 4 hrs. The fully swollen gel was subjected to the mechanical testing. Top. middle and bottom parts of the swollen gel were tested and proved to offer same and stable mechanical properties under compression.
  • Figure 7 illustrates the difference in polyHEMA SPH strength based on the temperature at which the SPH formation is started-
  • the polyHEMA SPH was prepared at a starting reaction temperature of 25 0 C or 60 0 C, as indicated.
  • the SPH was tested using a Chatillon TCD-200 digital mechanical tester.
  • the SPH was swollen using deionized water as the swelling medium at a temperature of 22-25 0 C
  • the SPH was retained in the swelling medium for 4 hrs .
  • Figure 8 illustrates the difference in polyHEMA SPH strength based on the temperature at which the SPH formation is started.
  • the polyHEMA SPH was exposed to the same reaction conditions as was the polyHEMA SPH of Figure 7, except that it was swollen in simulated gastric fluid at a pH of 1.0 at 37 0 C for 4 hr.
  • the polyHEMA SPH synthesized at a higher temperature is softer, deforms more but still is very strong.
  • the mechanical behavior of the gels synthesized at different temperatures was found to be very stable in both SGF and deionized water (see Figure 7).
  • the properties of the polyHEMA SPH are dependent on the starting reaction temperature, water content of the reacting mixture, and the foaming aid (e.g., acetic acid) concentration within the formulation.. Higher temperature, higher water content, and higher acid concentration result in taller foam, smaller pore size, more flexibility, more processability, and better swelling properties (see Figures 7-8).
  • Dissolution of the foaming agent increases the pH of the reaction medium to a level at which the initiator decomposes faster. As the formation of initiator radicals reaches a certain level, the polymerization reaction proceeds rapidly and the reacting mixture becomes viscous over time. Dissolution of the foaming agent also promotes its interaction with the foaming aid to produce gases required for the blowing process.
  • the two processes are conducted in such a way as to enable controlled foaming and polymerization.
  • t Q is the time at which the foaming agent was added
  • (D) symbols in the chart denote the degree of foaming
  • ( ⁇ ) symbols denote the temperature rise during the reaction.
  • a high or very high mechanical property can be achieved with SPHs in their fully-swollen state, if the SPH has a very homogeneous porous structure, as we have achieved A swollen SPH quickly fails under static and dynamic mechanical loading (compression, tension, bending, twisting) if the SPH possesses weak points like big pores, pores of different sizes or areas of different porosity (non-porous versus porous).
  • a premature gelation before foaming results in formation of hydrogel product lacking significant porosity rather than a superporous hydrogel rich in porosity.
  • a premature extensive foaming before gelation results in heterogeneous pore structure and size.
  • the method in which a foaming agent is added to the reaction mixture, its mixing with the reaction mixture, the reaction temperature, and the amount of diluent, foaming aid, and/oi foam stabilizer are critical factors to achieve harmonized foaming and gelation reactions.
  • PoIyHEMA SPHs are strong, demonstrating the ability to resist contractions imposed by the stomach of the patient, and exhibit excellent swelling properties, including a fast rate of swelling and the ability to absorb a large volume of fluid.
  • the SPHs need to be encapsulated in an orally administrable capsule (gelatin, HPMC for example),
  • the encapsulation of PoIyHEMA SPHs requires a further step of plasticization including use of external/internal plasticizers as well as moisture-
  • the general practice with external plasticizers is to soak the final purified and dried SPH in the plasticizer solution.
  • Figure 9 illustrates the different mechanical properties of a HEMA-based SPH and a polyHEMA/HEA SPH of the present invention (lower HEA concentration). As indicated, both SPHs exhibit similar excellent mechanical properties at a pH of 1.0
  • a wide range of SPHs having diverse mechanical properties can be prepared using mixed monomers of HEMA and HEA. While HEMA is responsible for the improved high mechanical properties of the SPH, the HEA provides better swelling properties, including an increase in the swelling rate and swelling capacity.
  • a flexibilized type of SPH can be obtained if the HEMA monomer is partially replaced by HEA as comonomer.
  • High temperature, high water content, and high HEA concentration all result in more flexibility in dry and in water-swollen state.
  • Increasing the HEA concentration produces a SPH having superior swelling properties at the expense of its mechanical properties
  • the HEA concentration can be preferably varied in the range of HEA/HEMA ratio of 0-50 v/v %, the most preferable concentration is around 25 v/v % ratio or less of HEA/HEMA.
  • the ratio of HEA to HEMA is 20 v/v %
  • pHEMA -AAc/AP* SPHs were left in ambient conditions for a few days and manually tested for hardness again.

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Abstract

Cette invention concerne des hydrogels superporeux modifiés (SPH) ainsi que des procédés permettant de les fabriquer. Les SPH décrits dans cette invention sont préparés par sélection soigneuse d'ingrédients réactifs hydrophiles/hydrophobes puis par harmonisation du moussage et des réactions de polymérisation, ce qui permet d'aboutir à la formation de SPH présentant une structure homogène ainsi que des propriétés mécaniques et physiques avantageuses, parmi lesquelles le gonflement, la résistance, la robustesse et l'élasticité. Les SPH décrits dans cette invention sont particulièrement utiles dans des environnements de gonflement acides, tels que l'environnement au pH basique du fluide gastrique contenu dans l'estomac, pendant des périodes prolongées.
PCT/US2007/072892 2006-07-06 2007-07-06 Hydrogels superporeux pour applications très résistantes WO2009029087A2 (fr)

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